Fuel cell using novel electrolyte membrane

ABSTRACT

Apparatus and method for producing electricity from a fuel gas containing hydrogen and/or compounds capable of dissociating into hydrogen ions using a solid electrolyte concentration cell and a catalyst. A novel solid electrolyte membrane is used which comprises an organic polymer-inorganic compound blend prepared by admixing an organic polymer such as poly(vinyl alcohol) with a heteropoly acid or salt thereof such as dodecamolybdophosphoric acid or uranyl orthophosphate in a mutually miscible solvent.

BACKGROUND OF THE INVENTION

This invention relates to a gaseous fuel cell. More specifically, it relates to the use of a novel solid electrolyte and a catalyst in producing electricity from hydrogen or gases capable of dissociating to yield hydrogen ions.

The Nernst equation provides a mathematical description of such a system, as follows. When two media with different partial pressures, P₁ and P₂, of a particular substance present in both media are separated by a solid electrolyte (ionic conductor) and conducting electrodes are attached to both sides of the ionic conductor, an EMF is generated which is related to the partial pressures as follows: ##EQU1## where R is the gas constant, T is absolute temperature, F is the Faraday constant, E_(o) is the standard oxidation-reduction potential difference, EMF is electromotive force, and n is the number of electrons per molecule of product from the overall cell reaction. If the system described by the above equation behaves non-ideally, the partial pressures must be replaced by fugacities. Another factor which may need to be considered in regard to a particular system is the rate of dissociation to form the ions which pass through the solid electrolyte. This may be a limiting factor to the transfer of ions through the electrolyte. The rate of dissociation can be calculated by means of the equilibrium constant for the dissociation reaction.

In a simple hydrogen-oxygen fuel cell, the fuel gas is hydrogen and the oxidant gas is oxygen. Hydrogen dissociates into hydrogen ions and electrons at the catalyst on the fuel gas side of the membrane. The hydrogen ions pass through the electrolyte element while the electrons flow through the external circuit, doing electrical work before forming water by combining with, at the catalytic agent on the oxidant gas side of the membrane, hydrogen ions which passed through the membrane and oxygen. A flow of gases is normally maintained for continuous operation of the fuel cell. The maximum voltage which can be produced by a fuel cell is a thermodynamic function of the fuel and oxidant. For a hydrogen-oxygen fuel cell at STP, the theoretical EMF is 1.23 volts. The actual voltage will be less due to losses within the cell. The current produced is controlled by such considerations as the rate at which the electrochemical reactions proceed, the electrolyte thickness, and the catalyst surface area. In a simple hydrogen-oxygen cell, the partial pressure term of the Nernst equation becomes partial pressure of water divided by the quantity partial pressure of hydrogen times square root of partial pressure of oxygen.

A novel solid electrolyte membrane is used in the present invention. We have discovered that a polymer blended membrane may be fabricated by admixing a heteropoly acid or a salt thereof with an organic polymer which is at least partially compatible with said heteropoly acid or salt to form a polymer blended composition of matter which is useful in gas detection. It was totally unexpected that a thin film membrane could be cast from such a blend to provide a membrane which would be highly selective to certain gases and therefore able to act as a proton conductor in a fuel cell where molecular hydrogen is converted into protons on one side of the device, transported through the membrane, and recombined as molecular hydrogen on the other side. The membrane is also useful with gases capable of dissociating into hydrogen ions. For background information relating to this aspect of the present invention, reference may be made to the book Solid Electrolytes and Their Applications, edited by Subbarao, Plenum Press, 1980. For information on fuel cells see Journal of the Electrochemical Society, March, 1978, p. 77C and U.S. Pat. No. 3,403,054 (Puffer et al.).

BRIEF SUMMARY OF THE INVENTION

It is among the objects of the present invention to provide an improved fuel cell utilizing a fuel gas comprising hydrogen or a gaseous component capable of dissociating into hydrogen ion.

The invention utilizes a concentration cell whose electrolyte is a thin film organic-inorganic membrane which conducts hydrogen ions. The membrane is mounted in a membrane housing having a fuel gas chamber and an oxidant gas chamber. The fuel gas chamber contains a gas comprising hydrogen or a component capable of dissociating to form hydrogen ions. In the other chamber is an oxidant gas which combines with hydrogen ions which have passed through the membrane. The membrane must be substantially imporous so that the two gases will not mix by diffusing through it. A catalytic agent for promotion of dissociation or combination is in intimate contact with the membrane on the sample gas side. Catalytic agent is also provided in a like manner on the other side. It is not necessary that the same catalytic agent be used on both sides. Means for forming electrical contact and transferring electrons to and from an external circuit are provided on each side of the electrolyte in intimate contact with catalytic agent. The EMF and current produced is generally in accordance with the parameters discussed above: the Nernst equation and, where applicable, the dissociation equilibrium constant. However, exact adherence to theoretical relationships is not required of commercially used methods and apparatus.

The method of the invention may be summarized as a method for producing electricity from a fuel gas having a gaseous component which is capable, in the presence of a catalytic agent, of dissociating to yield hydrogen ions, such method comprising contacting said fuel gas with a first surface of a thin film organic-inorganic membrane, contacting an oxidant gas with a second surface of said membrane, and forming an electrical connection between two separate portions of a catalytic agent effective to promote dissociation and combination, where one portion of catalytic agent is in contact with said first surface and one portion of catalytic agent is in contact with said second surface of said membrane, which membrane isolates fuel gas from oxidant gas, said membrane comprising a blend of a compound selected from the group consisting of heteropoly acids and salts thereof and a polymer which is at least partially compatible with said compound.

Temperature of the gas or gases and/or the membrane housing may be controlled at a pre-established value. The catalytic agent may be nickel, platinum, palladium, or alloys thereof. The catalytic agent may be electrically conductive. The form of the electrolyte element may require that gas which contacts it be dry or that at least one of the gases contain water vapor. The temperature of the fuel gas and/or oxidant gas may be adjusted before the gas is contacted with the electrolyte element.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic representation, in cross-section, of a test fixture used in initial proof of principle experimentation. The drawing is not to scale.

FIG. 2 depicts an embodiment of the invention, in a sectional view, in which a membrane is part of a partition separating a fuel gas chamber from an oxidant gas chamber.

DETAILED DESCRIPTION OF THE INVENTION

Before the development of the above-mentioned blended membrane, it was attempted to use a heteropoly acid, dodecamolybdophosphoric acid (DMPA) as a solid electrolyte in a system useful in gas detection and separation and power generation. The principles involved are basically the same. The Nernst equation is applicable. However, a difference is that in a gas detector, the external circuit is a measuring circuit rather than a flow path for electrons which will combine with substances at the catalyst. DMPA purchased in powder form from Alpha-Ventron was pressed at approximately 20,000 psi for about 20 seconds to form a wafer 1 inch in diameter and approximately 3 mm thick. It was necessary to use glass epoxy platens to prevent the DMPA from contacting the steel press dies in order to prevent formation of a blue liquid. Sputter deposition of platinum on the wafer to serve as catalyst was unsuccessful, first because a vacuum suitable for sputter deposition could not be obtained, apparently as a result of the water of hydration in the wafer, and then because the wafer developed cracks which made it unable to function as a gas impermeable barrier. A platinum-impregnated carbonaceous material was successfully fabricated as catalyst and electrode by placing it in the press dies and pressing it along with the DMPA. Impregnation was accomplished by adding chloroplatinic acid to carbonaceous material and decomposing to leave elemental platinum. However, use of this wafer in a gas detector suffered from a number of drawbacks, including brittleness of the wafer and difficulty in making good electrical contact between the electrodes and DMPA. Another serious problem was that the amount of water vapor in the gas contacting the wafer had to be maintained in a narrow range to prevent deterioration of the wafer. With too much water, the wafer became spongy and with too little, it cracked. Attention was then directed toward other substances and a novel substance useful in gas detection and separation and fuel cells was discovered.

When attempting to blend an organic polymer with an inorganic compound, the usual result is to obtain a phase separation. In contradistinction to this, we have discovered that a single phase system may be obtained by admixing certain organic polymeric compounds with a heteropoly acid or salt thereof, the resulting composition of matter forming a thin film membrane which may be utilized in this invention. The use of these membranes is due in some respect to the fact that heteropoly acids or salts thereof possess a high protonic conductivity, especially at room or ambient temperature. The membranes which are formed from the blend of the organic polymer and the heteropoly acid or salt thereof possess excellent transport properties as well as an increase in tensile strength over those membranes prepared from pure organic polymers. The physical properties which these thin film membranes exhibit thus provide an attractive base for their use in the present invention. As will hereinafter be shown in greater detail, the organic-inorganic blends possess chemical, mechanical and electrical properties which indicate the two materials form a single phase system. For example, the blends possess only one glass transition temperature, which indicates a single phase system inasmuch as, if the resulting membranes were a two-phase system, or merely a physical mixture, the composition would possess two separate and distinct glass transition temperatures. In addition, the yield strength and modulus is greatly increased over those properties which are possessed by either of the two components. Another physical characteristic which indicates a single phase or true composition of matter is that the blend is transparent to visible light as well as being uniform in color.

The desired membrane comprises a blend of an organic polymer and a heteropoly acid or salt thereof, the polymer being at least partially compatible with the acid or salt. Examples of organic polymers which may be employed as one component of the blend of the present invention include poly(vinyl alcohol) (PVA), poly(vinyl fluoride), polyethylene oxide, polyethyleneimine, polyacrylic acid, polyethylene glycol, cellulose acetate, polyvinylmethylethyl ether, phenol formaldehyde resins, etc.

Examples of heteropoly acids or salts thereof which may be employed as the second component of the organic-inorganic blend which may be used to form a membrane will possess the generic formula:

    A.sub.m[X.sub.x Y.sub.y O.sub.z ].nH.sub.2 O

in which X and Y may be selected from the group consisting of boron, aluminum, gallium, silicon, germanium, tin, phosphorus, arsenic, antimony, bismuth, selenium, tellurium, iodine, and the first, second, third and fourth transitional metal series, said series including scandium, yttrium, lanthanum, actinium, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum and tungsten, X and Y being dissimilar in nature, A is selected from the group consisting of hydrogen, ammonium, sodium, potassium, lithium, rubidium, cesium, beryllium, magnesium, calcium, strontium and barium, m is an integer of from 1 to 10, y is an integer of from 6 to 12 based on x taken as 1, z is an integer of from 30 to 80 and n is an integer of from 3 to 100.

Specific examples of these compounds will include dodecamolybdophosphoric acid (DMPA), ammonium molybdophosphate, sodium molybdophosphate, potassium molybdophosphate, lithium molybdophosphate, calcium molybdophosphate, magnesium molybdophosphate, dodecatunstophosphoric acid, ammonium tungstophosphate, sodium tungstophosphate, potassium tungstophosphate, lithium tungstophosphate, calcium tungstophosphate, magnesium tungstophosphate, dodecamolybdosilicic acid, ammonium molybdosilicate, sodium molybdosilicate, potassium molybdosilicate, lithium molybdosilicate, calcium molybdosilicate, magnesium molybdosilicate, dodecamolybdogermanic acid, ammonium molybdogermanate, sodium molybdogermanate, potassium molybdogermanate, lithium molybdogermanate, calcium molybdogermanate, magnesium molybdogermanate, hexamolybdotelluric acid, ammonium molybdotellurate, sodium molybdotellurate, potassium molybdotellurate, lithium molybdotellurate, calcium molybdotellurate, magnesium molybdotellurate, dodecatungstosilicic acid, ammonium tungstosilicate, sodium tungstosilicate, potassium tungstosilicate, lithium tungstosilicate, calcium tungstosilicate, magnesium tungstosilicate, etc. It is also contemplated within the scope of this invention that some uranyl compounds may also be employed as the heteropoly acid or salt thereof. These uranyl compounds will possess the generic formula:

    A[UO.sub.2 ]XO.sub.4.nH.sub.2 O

in which A is selected from the group consisting of hydrogen, lithium, sodium, potassium, ammonium, copper, magnesium, calcium, barium, strontium, lead, iron, cobalt, nickel, manganese, and aluminum, X is selected from the group consisting of phosphorus and arsenic and n is an integer of from 1 to 4. Some specific examples of these uranyl compounds will include uranyl orthophosphate (HUOP), uranyl orthoarsenate, lithium uranylphosphate, lithium uranylarsenate, sodium uranylphosphate, sodium uranylarsenate, potassium uranylphosphate, potassium uranylarsenate, ammonium uranylphosphate, ammonium uranylarsenate, calcium uranylphosphate, calcium uranylarsenate, barium uranylphosphate, barium uranylarsenate, copper uranylphosphate, copper uranylarsenate, iron uranylphosphate, iron uranylarsenate, cobalt uranylphosphate, cobalt uranylarsenate, nickel uranylphosphate, nickel uranylarsenate, etc.

It is to be understood that the aforementioned listing of organic polymeric compounds, heteropoly acids or salts thereof are only representative of the class of compounds which may be employed in formulating the organic-inorganic blends used in the present invention.

The membranes used in the present invention are prepared by admixing the two components of the blend in a mutually miscible solvent at reaction conditions for a period of time sufficient to form the desired blend. In the preferred membrane, the mutually miscible solvent which is employed to dissolve the components comprises water, although it is contemplated that any other mutually miscible solvent, either inorganic or organic in nature may also be employed. The mixing of the two components of the membrane may be effected at reaction conditions which will include a temperature in the range of from about ambient (20°-250° C.) up to the boiling point of the mutually miscible solvent which, for example, in the case of water is 1OO° C. The time of reaction which is necessary to form the desired blend will vary with the particular organic polymers and heteropoly acids or salts thereof as well as the solvent and may be within a period of time ranging from about 0.5 up to about 10 hours or more in duration. Upon completion of the reaction period, the blend is cast upon a suitable casting surface which may consist of any suitable material sufficiently smooth in nature so as to provide a surface free of any defects which may cause imperfections on the surface of the membrane. Examples of suitable casting surfaces may include metals such as stainless steel, aluminum, etc., glass, polymer or ceramics. After casting the solution upon the surface, the solvent is then removed by any conventional means including natural evaporation or forced evaporation by the application of elevated temperatures whereby said solvent is evaporated and the desired membrane comprising a thin film of the polymeric blend is formed. In the preferred membrane, the polymeric blend of an organic-inorganic compound will possess a molecular weight ranging from about 2000 up to about 135,000 and preferably greater than 10,000. The thickness of the film can be controlled by the amount of polymer and heteropoly acid or salt thereof which is present in the reaction mixture. In this respect, it is to be noted that the ratio of heteropoly acid or salt and organic polymer may vary over a relatively wide range. For example, the heteropoly acid or salt may be present in the blend in a range of from about 1% to about 70% by weight of the blend while the organic polymer may be present in an amount in the range of from about 99% to about 30% by weight of the blend. Initially, it was believed that the ranges were narrower; about 10% to about 70% for the heteropoly acid on salt and about 90% to about 30% for the organic polymer. The thin film organic-inorganic blend which is prepared according to the process of the present invention will possess a thickness which may range from about 0.1 to about 50 microns and preferably from about 5 to about 20 microns.

The polymer blend membranes may be prepared by placing a predetermined amount of each of the components of the blend, namely, the organic polymer and the heteropoly acid or salt thereof, in an appropriate apparatus such as a flask. After adding the mutually miscible solvent, the mixture is allowed to remain, after thorough admixing thereof, for a predetermined period of time within the range hereinbefore set forth. As an example, poly(vinyl alcohol) and dodecamolybdophosphoric acid may be placed in a flask and dissolved in water which has been heated to 1OO° C. Upon completion of the desired residence time, the solution is cast upon an appropriate casting surface and the water or other solvent is removed. The desired and resulting polymer blend membrane is then recovered and utilized in gas separation (etc.).

Examples of novel thin film organic-inorganic polymer blends which may be prepared include poly(vinyl alcohol)-dodecamolybdophosphoric acid, poly(vinyl fluoride)-dodecamolybdophosphoric acid, cellulose acetate-dodecamolybdophosphoric acid, polyethylene oxidedodecamolybdophosphoric acid, polyethylene glycol-dodecamolybdophosphoric acid, poly(vinyl alcohol)-dodecatungstophosphoric acid, poly(vinyl fluoride)-dodecatungstophosphoric acid, cellulose acetate-dodecatungstophosphoric acid, polyethylene oxide-dodecatungstophosphoric acid, polyethylene glycol-dodecatungstophosphoric acid, poly(vinyl alcohol)-dodecamolybdosilicic acid, poly(vinyl fluoride)-dodecamolybdosilicic acid, cellulose acetate-dodecamolybdosilicic acid, polyethylene oxide-dodecamolybdosilicic acid, polyethylene glycol-dodecamolybdosilicic acid, poly(vinyl alcohol)-ammonium molybdophosphate, poly(vinyl fluoride)-ammonium molybdophosphate, cellulose acetate-ammonium molybdophosphate, polyethylene oxide-ammonium molybdophosphate, polyethylene glycol-ammonium molybdophosphate, poly(vinyl alcohol)-uranyl orthophosphate, poly(vinyl fluoride)-uranyl orthophosphate, cellulose acetate-uranyl orthophosphate, polyethylene oxide-uranyl orthophosphate, polyethylene glycol-uranyl orthophosphate, etc. It is to be understood that the aforementioned list of polymer blends is only representative of the class of polymer blend membranes which may be prepared.

It will be helpful in gaining an understanding of the invention to examine initial proof of principle experimentation. The information presented in regard to this experimentation is not meant to limit the scope of the invention in any way. As mentioned above, this experimentation was directed to obtaining information on gas detection and separation, as well as fuel cells.

A novel polymer blend membrane was prepared by dissolving poly(vinyl alcohol) and dodecamolybdophosphoric acid in boiling deionized water, the amount of organic polymer and heteropoly acid being sufficient to impart a 50/50 weight percent ratio to the resulting polymer blend membrane. The solution was then poured into an evaporation dish and the water was allowed to evaporate for a period of 16 hours. The resulting blended film was yellow-green in color and possessed a thickness of 20 microns.

Various analyses of the film were performed to determine whether or not the film was in single-phase or two-phase. The blended film was found to be optically transparent, and no phase separation was observed when the film was examined with an optical microscope or SEM. The specimen was also subjected to a glass transition temperature measurement inasmuch as the measurement of the glass transition temperature, or temperatures, of a polymer blend is the most commonly used criteria for determining the number of phases present in a blend. For example, a single-phase organic-inorganic blend will exhibit a single glass transition temperature between the temperatures of the components, while in a two-phase system, two separate temperatures will result. Poly(vinyl alcohol) has a known glass transition temperature of about 71° C., while the melting point temperature of dodecamolybdophosphoric acid is about 84° C. A DSC scan of the film prepared according to the above paragraphs had a peak of 78° C. while no peaks were observed at temperatures corresponding to the glass transition temperatures of poly(vinyl alcohol) or the melting point of dodecamolybdophosphoric acid.

Infrared spectroscopy of the film showed four strong bands appearing at 820 cm⁻¹, 885 cm⁻¹, 972 cm⁻¹, and 1075 cm⁻¹. The indication from this analysis is that the bands are associated with intermolecular bonding between the poly(vinyl alcohol) and the dodecamolybdophosphoric acid. In addition to these analyses, it was found that the blended film possessed increased tensile strength and modulus over that which is possessed by either poly(vinyl alcohol) or dodecamolybdophosphoric acid, the increase in tensile strength and modulus perhaps being the result of increased hydrogen bonding due to the formation of a single phase material.

The thin film membrane was cut into a disc having a 1" diameter to form membrane 1 of FIG. 1 and platinum was sputter-deposited onto both sides of the disc. The deposited platinum disc had a thickness ranging from about 100 to about 200 angstroms and a diameter of about 1.2 cm. Deposition was accomplished by means of a Hummer II sputter deposition system supplied by Technics Co. The first few attempts at platinum sputter deposition resulted in degradation of the PVA/DMPA film due to excessive electron bombardment. To reduce the flux of electrons striking the film, the biasing configuration of the sputter deposition system was changed. The addition of a biased screen between the target and film reduced the electron flux to the membrane and permitted metal to be deposited without damage. There are many alternative methods which could have been used to form the platinum deposits, such as thermal evaporation or deposition by means of an ink. The porous structure of sputter deposited catalytic agent is helpful in facilitating spillover of hydrogen ions onto the membrane, but it is not required. Note that hydrogen will migrate through solid platinum.

Referring to FIG. 1, membrane 1 was mounted in test fixture 2, which may also be referred to as a sample cell, membrane housing, or test sensor. The above mentioned platinum deposits 5 served as catalytic agent to promote dissociation and re-association. Electrical contact was made to the platinum through copper platens 6, which were held in place by springs (not shown) extending between the platens and interior surfaces of the sample cell. Platens 6 did not cover the entire surface of the catalytic agent, though FIG. 1 shows this to be the case. Note that when the catalytic agent is electrically conductive and not discontinuous, electrical contact need be made only at one point. Wire leads 3 and 4 extended from the platens out of the test fixture through means for sealing against gas leakage (not shown). Leads 3 and 4 were connected to EMF and current detection means (not shown). Membrane 1 was sealed into test fixture 2 by O-rings 7 so that there were no gas leakage paths between test gas chamber 8 and reference gas chamber 9 (which may also be referred to as fuel gas chamber and oxidant gas chamber). Tubing (not shown) was connected at gas inlets 10 and 11 to provide gas flow into chambers 8 and 9 and was also connected to gas outlets 12 and 13 to conduct gas away from the chambers. Gas cylinders and gas mixing and flow control apparatus (not shown) were used to provide gas to test fixture 2 in accordance with the herein described experiments. It must be noted that the gas mixing apparatus was capable of accuracy suitable for proof of principle experimentation but not for more rigorous work. Also, no attempt was made to separately analyze the gas mixtures prepared by diluting purchased gas.

Gas flows were established through the chambers of the sample cell with both chamber pressures at essentially one atmosphere, since the chambers were vented directly to atmosphere. One flow was pure hydrogen (hydrogen partial pressure of approximately 1.0 atm.) and the other was a 2% by volume mixture of hydrogen in nitrogen (hydrogen partial pressure of approximately 0.02 atm.). The gas flows were alternated between test gas chamber 8 and reference gas chamber 9 and the voltage across wires 3 and 4 was recorded by means of a standard laboratory strip chart recorder. The reproducibility and accuracy was very good. Voltage varied consistently between positive 49.5 millivolts and negative 49.5 mv. Response was Nernstian; the calculated voltage is also 49.5 mv (at a room temperature of 22° C.). Hydrogen flux and current flow were also determined.

Membranes having other amounts of PVA and DMPA were prepared and tested in the same manner as described above for the 50/50 weight percent blend. PVA is commercially available in several nominal molecular weights (MW). Most membranes were prepared with PVA of MW 78,000, though MW 16,000 and 133,000 were also used. Following is a tabulation of data for several membranes with varying blends by weight percent and using a reference to sample gas hydrogen pressure ratio of 100:2. Current (I) is in milliamps. Hydrogen flux is in ft.³ /ft.² -hr. times 10⁻³.

    ______________________________________                                         PVA/DMPA         I       Flux                                                  ______________________________________                                         90/10            0.0005  0.0056                                                75/25            0.031   0.339                                                 50/50            0.1337  1.46                                                  40/60            0.1337  1.46                                                  ______________________________________                                    

The same open-circuit voltage (49.5 mv) was observed for each of the last three blends above. Reproducibility of measurements taken for the 90/10 blend was not good, leading to the conclusion that the maximum amount of PVA usable with DMPA is about 90% by weight. With DMPA contents above about 70% by weight, the membranes were brittle and also appeared to form a two-phase system.

With a PVA/DMPA membrane, it is necessary that some significant amount of water vapor be present in either the sample gas stream or the reference gas stream or both. The amount of water vapor is not critical, as it was in the case of the pressed DMPA wafer, but some is required for the detector to operate properly. In the tests performed, the smallest amount of water vapor used was that needed to cause a relative humidity of about 30% in the gas stream. It is expected that the minimum amount required is at least an order of magnitude less.

In addition to platinum, gold and palladium were deposited on membranes for use as catalytic agent. Nernstian voltage response was observed when palladium was used. Switching gas streams as described above but using a 75/25 membrane with sputter-deposited palladium yielded a strip chart record indistinguishable from that mentioned above. Gold electrodes were ineffective; no meaningful voltage response to hydrogen partial pressure was observed. This was not unexpected, as gold, unlike platinum and palladium, does not dissociate molecular hydrogen at room temperature. It is expected that nickel will be effective as catalytic agent if it is desired to utilize the invention at higher temperatures, since nickel is known to dissociate hydrogen at higher temperatures. Other catalytic agents are available and known to those skilled in the art. The catalytic agent need not be electrically conductive; however, then the means for forming electrical connection must be in contact with the catalytic agent over a broad area, to faciliate movement of electrons from sites of the catalytic agent to the electrically conductive substance, or electrode. Areas of membrane which are not adjacent to catalytic agent are not effective in the invention. Hydrogen ions spill over from the catalytic agent to the membrane and then the protons move through the membrane.

Gases other than nitrogen were used to dilute hydrogen passed through the test fixture. Use of helium resulted in no change at all in measured voltages. The presence of small amounts of carbon monoxide (less than 5% by volume) in a 2% hydrogen (by volume) in nitrogen sample gas stream with a 100% hydrogen reference gas stream caused a change in EMF indicative of a large reduction in hydrogen partial pressure. This apparent drop in hydrogen concentration was much larger than the expected drop due to the effect of dilution of sample gas with CO. This is likely due to the competition by CO with molecular hydrogen for adsorption sites on platinum and palladium. The invention cannot be used where CO, or other substances which interfere in the same manner, is present, unless the amount of CO, or other substance, is small.

In further detector-oriented experimentation, sample gas streams of lower hydrogen partial pressure were passed through the test fixture, the reference gas being pure hydrogen. The membrane used was 75% PVA/25% DMPA with palladium catalyst. Observed EMF (mv) and theoretical EMF (mv), as calculated by the Nernst equation, are as follows for several hydrogen concentrations (expressed in parts per million).

    ______________________________________                                         Concentration   Observed Theoretical                                           ______________________________________                                         20,000          49       49                                                    10,000          56       58                                                     2,500          77       77                                                     1,000          88       88                                                    ______________________________________                                    

It was not possible to check lower concentrations due to limitations of the gas mixing equipment. It is believed that the value of 56 mv, above, is due to a mixture which varied from 10,000 ppm.

Response time of a sensor with a 40% PVA/60% DMPA membrane having platinum catalyst was tested. When the 100% and 2% gas streams were switched between chambers as described above, the time required for the voltage to change from 10% to 90% of its final value was approximately 6 seconds. The time required to trace about 80% of the length of a similar curve was about 6 seconds. It should be noted that the sample cell used is not necessarily designed for quick response.

The above description of the invention has dealt with hydrogen. It is obvious that any substance capable of dissociating in the presence of a catalyst to yield hydrogen ions may be the operative component in a fuel gas mixture. Examples are ammonia, methanol, and fuel gas derived from such traditional fuels as coal and fluid hydrocarbons. The Nernst equation applies in a manner similar to that described above.

Membranes of PVA and uranyl orthophosphate (HUOP) were made and tested in the apparatus of FIG. 1 after platinum was sputter-deposited on them. In every case, the blend was prepared with equal weights of PVA and HUOP (before further treatment). PVA of three different molecular weights was used. PVA and HUOP were mixed with water and cast in the same manner as described above. Since HUOP is slightly soluble in water, large amounts of HUOP remained undissolved in the solutions prepared. Before casting, some solutions were filtered through Sargent-Welch S-32915-D filter paper, some were filtered through a 0.22 micron (nominal rating) Millipore filter, and those of one PVA molecular weight only (16,000) were ultracentrifuged for 30 minutes. In most cases, the membranes exhibited Nernstian behavior. The following table summarizes the results for the various membranes, including those cast without filtering or ultracentrifuging. N denotes Nernstian response and non-N denotes non-Nernstian response. A dash denotes that the combination was not tested.

    ______________________________________                                                  Molecular Weight                                                      Treatment  16,000       78,000  133,000                                        ______________________________________                                         None       Non-N        N       Non-N                                          S-W Filter N            N       Non-N                                          Millipore  N            N       N                                              Centrifuge N            --      --                                             ______________________________________                                    

The following information was developed using only membranes cast with PVA/HUOP solutions after passage through the Millipore filter and a reference gas of pure hydrogen flowing through reference gas chamber 9 of test fixture 2 (FIG. 1). Using a membrane comprising PVA of 16,000 MW and switching the sample gas between 100% hydrogen and 20% hydrogen, an EMF curve similar to FIG. 2 resulted. The voltage varied between 0 and -18.5 mv instead of the -20.5 mv predicted by the Nernst equation. With a 78,000 MW PVA membrane and a 0.1% hydrogen stream, there was a difference of 0.2 mv between the recorded EMF and the theoretical of -87.8 mv. With a 133,000 MW PVA membrane and a 20% hydrogen stream, there was a difference of 0.2 mv between the recorded EMF and the theoretical of -20.5 mv. In each of these three cases, it appears that the response time is faster when the sample gas concentration is switched to 100% hydrogen than when it is switched to the lower hydrogen concentration. This is apparent from the strip chart recorder tracing (not shown herein) because there are square corners at the 0 voltage line and completely horizontal lines traced at 0 voltage, in contrast to the rounded approach to the lower EMF values. The cause of this behavior has not yet been determined. A 78,000 MW PVA membrane was used in taking EMF readings with sample gases of concentrations from 100% hydrogen to approximately 300 ppm hydrogen. A plot of EMF versus ln(hydrogen concentration) yielded a straight line with a slight curve at the low concentration end. We are convinced that the response is linear and the deviation shown by the curve was due to equipment limitations at low concentrations. A system was tested continuously for 96 hours, with the sample gas being switched from 100% to 0.1% hydrogen and vice versa every 20 minutes. The strip chart recorder tracing for the first hour was the same as that for the last hour. There was no drift of baseline, change in EMF, or change in response time. In all of the experimentation with PVA/HUOP membranes, no water vapor was added to either the reference gas or the sample gas. The purchased gas, before dilution, contained a maximum of 20 ppm water. It can thus be concluded that the presence of water vapor is not required with this particular blend, as it is when using a PVA/DMPA blend in a sensor, or sample cell.

As mentioned above, large quantities of HUOP remained undissolved, leading to a brief investigation of the amount of HUOP in the membrane. The results were that membranes containing as little as 1% by weight HUOP were prepared.

The following table gives the results of experimentation accomplished in the same general manner as above, using air as the oxidant gas and pure hydrogen as the fuel gas. Platinum catalyst/electrode material was used in a thickness of 200-300 angstroms on each side of a PVA/DMPA membrane. Several PVA molecular weights were used. The amounts of PVA and DMPA are shown. Open circuit EMF (V) given in volts. Closed circuit density current (C) is given in milliamps per square centimeter.

    ______________________________________                                         mw       PVA/DMPA         V      C                                             ______________________________________                                         16,000   75/25            0.912  0.6                                           16,000   50/50            0.895  5.0                                           16,000   40/60            0.870  1.6                                           10,000   90/10            0.935  0.03                                          10,000   75/25            0.912  1.3                                           10,000   50/50            0.800  6                                             10,000   40/60            0.365  2                                             78,000   50/50            0.865  1.4                                           ______________________________________                                    

Open current voltage behavior is excellent; a typical hydrogen-oxygen fuel cell will display values from 0.6 to 0.85 volts. If pure oxygen had been used as an oxidant gas instead of air, the open circuit voltage would have been higher. No attempts were made to optimize performance.

A fuel gas may have only one component or more than one. Sample cell or membrane housing or test fixture refers to a housing or fixture which holds an electrolyte element and other required components. FIG. 2 depicts a membrane housing. Sensor is a general term denoting sensing apparatus, such apparatus comprising a membrane housing. Membrane or electrolyte element refers to an ion conducting substance suitable for use as an electrolyte in the concentration cell of this invention which has been formed into a particular physical entity, either with or without additional substances, for use in the invention. Where an electrolyte element surface is referred to as in common with a gas or gas chamber, the meaning is the same as exposed to a gas or gas chamber and such reference does not preclude the presence of catalytic agent and electrodes at or covering the surface. Gas may diffuse through covering material. Gas chamber refers to any space in which gas which is involved in this invention exists. The term "gas" is used herein to include vaporized liquids regardless of boiling point characteristics of the substance. As used herein, miscible means capable of being mixed where there may only be a very small degree of solubility.

The design of fuel cells is well known. Many configurations are possible; FIG. 1 provides an example of one type. FIG. 2 depicts an embodiment of the invention in which membrane 66 serves as a part of partition 65. Partition 65 separates a fuel gas chamber from an oxidant gas chamber. Electrically conductive catalytic agent is present on both sides of membrane 66, as shown by reference numbers 67 and 68. Wire leads 53 and 54 extend to connection to electricity utilizing means (not shown). 

We claim as our invention:
 1. An apparatus for producing electricity from a fuel gas having a gaseous component which is capable, in the presence of a catalytic agent, of dissociating to yield hydrogen ions comprising:(a) a thin film organic-inorganic membrane which comprises a single phase blend of (1) from about 1% to about 70% by weight of a heteropoly acid and salts thereof having the generic formula:

    A.sub.m [X.sub.x Y.sub.y O.sub.z ].nH.sub.2 O

in which X and Y are selected from the group consisting of boron, aluminum, gallium, silicon, germanium, tin, phosphorus, arsenic, antimony, bismuth, selenium, tellurium, iodine, and the first, second, third and fourth transition metal series of the Periodic Table and where Y is dissimilar from X, A is selected from the group consisting of hydrogen, ammonium, sodium, potassium, lithium, rubidium, cesium, beryllium, magnesium, calcium, strontium and barium, m is an integer of from 1 to 10, y is an integer of from 6 to 12 based on x taken as 1, z is an integer of from 30 to 80 and n is an integer of from 3 to 100 and, (2) from about 99% to about 30% by weight of a polymer compatible with said heteropoly acid or salt thereof selected from the group consisting of poly(vinyl alcohol), poly(vinyl fluoride), polyethylene oxide, polyethyleneimine, polyacrylic acid, polyethylene glycol, cellulose acetate, polyvinylmethylethyl ether and phenol formaldehyde resins; (b) a membrane housing comprising a fuel gas chamber and an oxidant gas chamber separated by a substantially imporous partition comprising said membrane defined in element (a), said membrane having a first surface in communication with said fuel gas chamber and a second surface in communication with said oxidant gas chamber; (c) two separate portions of catalytic agent effective to promote dissociation and combination, one portion in contact with said first surface of said membrane and one portion in contact with said second surface of said membrane; and, (d) means for forming electrical connection in operative contact with said catalytic agent in contact with said first surface of said membrane and in operative contact with said catalytic agent in contact with said second surface of said membrane.
 2. The apparatus of claim 1 further characterized in that said catalytic agent is selected from a group consisting of platinum, nickel, palladium, and alloys thereof.
 3. The apparatus of claim 1 further characterized in that said catalytic agent is electrically conductive.
 4. The apparatus of claim 1 further characterized in that said catalytic agent is porous to said gaseous component.
 5. The apparatus of claim 1 further including means to adjust the operating temperature of said membrane housing.
 6. The apparatus of claim 1 further including means to supply fuel gas to the fuel gas chamber and oxidant gas to the oxidant gas chamber.
 7. The apparatus of claim 1 further including means to utilize electricity connected between said means for forming electrical connection.
 8. The apparatus of claim 7 further comprising means for maintaining the equilibrium hydrogen partial pressure associated with the fuel gas at a value higher than the equilibrium hydrogen partial pressure in the oxidant gas chamber.
 9. The apparatus of claim 1 in which said thin-film organic-inorganic membrane possesses a thickness of from about 0.1 to about 50 microns.
 10. The apparatus of claim 1 in which in said membrane said polymer comprises poly(vinyl alcohol) and said heteropoly acid comprises dodecamolybdophosphoric acid.
 11. A method for producing electricity from a fuel gas having a gaseous component capable of, in the presence of a catalytic agent, dissociating to yield hydrogen ions which comprises contacting said fuel gas with a first surface of a thin film organic-inorganic membrane, contacting an oxidant gas with a second surface of said membrane, wherein said membrane comprises a single phase blend of:a thin film organic-inorganic membrane which comprises a blend of (1) from about 1% to about 70% by weight of a heteropoly acid and salts thereof having the generic formula:

    A.sub.m [X.sub.x Y.sub.y O.sub.z ].nH.sub.2 O

in which X and Y are selected from the group consisting of boron, aluminum, gallium, silicon, germanium, tin, phosphorus, arsenic, antimony, bismuth, selenium, tellurium, iodine, and the first, second, third and fourth transition metal series of the Periodic Table and where Y is dissimilar from X, A is selected from the group consisting of hydrogen, ammonium, sodium, potassium, lithium, rubinidium, cesium, beryllium, magnesium, calcium, strontium and barium, m is an integer of from 1 to 10, y is an integer of from 6 to 12 based on x taken as 1, z is an integer of from 30 to 80 and n is an integer of from 3 to 100 and, (2) from about 99% to about 30% by weight of a polymer compatible with said heteropoly acid or salt thereof selected from the group consisting of poly(vinyl alcohol), poly(vinyl fluoride), polyethylene oxide, polyethyleneimine, polyacrylic acid, polyethylene glycol, cellulose acetate, polyvinylmethylethyl ether and phenol formaldehyde resins and said membrane is substantially impervious to said fuel gas and said oxidant gas, and forming an electrical connection between two separate portions of a catalytic agent effective to promote said dissociation and combination, wherein one portion of said catalytic agent is in contact with said first surface and one portion of said catalytic agent is in contact with said second surface of said membrane and wherein said membrane isolates said fuel gas from said oxidant gas.
 12. The method of claim 11 further characterized in that said gaseous component is hydrogen.
 13. The method of claim 11 further characterized in that the oxidant gas contains oxygen.
 14. The method of claim 11 further characterized in that water is added to the fuel gas the oxidant gas or both before the gas contacts said membrane.
 15. The method of claim 11 further characterized in that the oxidant gas is air.
 16. The method of claim 11 further characterized in that the temperature of the fuel gas, the oxidant gas or both is adjusted before said gas contacts said membrane.
 17. The method of claim 11 further characterized in that the equilibrium partial pressure associated with the fuel gas is maintained at a value higher than the equilibrium hydrogen partial pressure of the oxidant gas. 